CN114397922A - Temperature control system of carbon dioxide capture reboiler of coal-fired power plant - Google Patents

Temperature control system of carbon dioxide capture reboiler of coal-fired power plant Download PDF

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Publication number
CN114397922A
CN114397922A CN202111153018.1A CN202111153018A CN114397922A CN 114397922 A CN114397922 A CN 114397922A CN 202111153018 A CN202111153018 A CN 202111153018A CN 114397922 A CN114397922 A CN 114397922A
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reboiler
temperature
controller
input
outlet
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CN114397922B (en
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韩新宇
吴南翔
柳佳杰
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Beijing Yuancarbon Environment Co ltd
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Beijing Bezenith Energy Technology Co ltd
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    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D23/00Control of temperature
    • G05D23/19Control of temperature characterised by the use of electric means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01BBOILING; BOILING APPARATUS ; EVAPORATION; EVAPORATION APPARATUS
    • B01B1/00Boiling; Boiling apparatus for physical or chemical purposes ; Evaporation in general

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  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Automation & Control Theory (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention discloses a temperature control system of a carbon dioxide capturing reboiler of a coal-fired power plant, which comprises a steam input pipeline, a temperature regulating valve, a reboiler, a regeneration tower and a reboiler temperature controller, wherein the steam input pipeline is connected with the temperature regulating valve; the outlet at the bottom of the regeneration tower is communicated with the inlet of the reboiler through a reboiler pump, a thermometer is arranged at the outlet of the reboiler, the output end of the thermometer is connected with the input end of a reboiler temperature controller, the output end of the reboiler temperature controller is connected with the control end of a temperature regulating valve and the control end of the reboiler pump, and the system can effectively control the temperature of the reboiler.

Description

Temperature control system of carbon dioxide capture reboiler of coal-fired power plant
Technical Field
The invention belongs to the field of automatic control, and relates to a temperature control system of a carbon dioxide capturing reboiler of a coal-fired power plant.
Background
The coal-fired power plant serving as a carbon dioxide emission amplifying user faces huge challenges, the carbon dioxide capturing technology after combustion of the coal-fired power plant is widely researched and popularized at home and abroad at present, but the problem of overlarge capturing energy consumption exists at the same time, the temperature control of a carbon dioxide capturing reboiler of the power plant directly influences the energy consumption of the whole capturing system, and the temperature of the reboiler cannot be effectively controlled in the prior art, so that the energy consumption of the capturing system is seriously influenced.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provides a temperature control system of a carbon dioxide capturing reboiler of a coal-fired power plant, which can effectively control the temperature of the reboiler.
In order to achieve the aim, the temperature control system of the carbon dioxide capturing reboiler of the coal-fired power plant comprises a steam input pipeline, a temperature regulating valve, a reboiler, a regeneration tower and a reboiler temperature controller;
the outlet at the bottom of the regeneration tower is communicated with the inlet of the reboiler through a reboiler pump, a thermometer is arranged at the outlet of the reboiler, the output end of the thermometer is connected with the input end of a reboiler temperature controller, and the output end of the reboiler temperature controller is connected with the control end of a temperature regulating valve and the control end of the reboiler pump.
A pressure gauge is arranged in the regeneration tower, and the output end of the pressure gauge is connected with the input end of the reboiler temperature controller.
The reboiler temperature controller comprises a temperature setting correction value input end, a manual/automatic switching button, a reboiler temperature manual setting input end, a function module, a filtering module, an adder, a limiting module, a manual/automatic switching device, a PID controller and a split-range controller;
the output of pressure gauge is connected with the input of function module, and the output of function module and temperature setting correction value input are connected with the input of adder, and the output of adder is connected with the input of amplitude limiting module, and the output of amplitude limiting module is connected with the input of PID controller, and the output of PID controller is connected with the input of split-range controller, and the output of split-range controller is connected with the control end of temperature regulator valve and the converter of reboiler pump.
The output end of the function module is connected with the input end of the filtering module, and the output end of the filtering module and the input end of the temperature setting correction value are connected with the input end of the adder.
The output end of the amplitude limiting module and the manual temperature setting input end of the reboiler are connected with the input end of a manual/automatic switcher, and the output end of the manual/automatic switcher is connected with the input end of the PID controller.
The manual/automatic switching button is connected with the control end of the manual/automatic switcher.
When the device works, the pressure gauge measures the pressure information of the regeneration tower, the pressure information is calculated by the function module to obtain the temperature control target value information, the temperature control target value information is filtered by the filtering module to avoid the adjustment fluctuation caused by small pressure fluctuation, the filtered temperature control target value information and the temperature setting correction value are added by the adder and then subjected to amplitude limiting processing by the amplitude limiting module, then the temperature of the reboiler outlet is input into a manual/automatic switcher to be used as a target value of the reboiler outlet temperature, the target value of the reboiler outlet temperature and the temperature of the reboiler outlet measured by a thermometer are subjected to PID operation through a PID controller, and finally, controlling the opening of the temperature regulating valve and the rotating speed of a reboiler pump through the split controller, so that the temperature of the reboiler outlet is consistent with the target value of the temperature of the reboiler outlet.
The user inputs the target value of the reboiler outlet temperature into the manual/automatic switcher through the reboiler temperature manual setting input end, the target value of the reboiler outlet temperature and the temperature of the reboiler outlet obtained by measurement of the thermometer carry out PID operation through the PID controller, then the result of the PID operation is input into the split controller to be processed, and finally the opening degree of the temperature regulating valve and the rotating speed of the reboiler pump are controlled through the split controller, so that the temperature of the reboiler outlet is consistent with the target value of the reboiler outlet temperature, and the aim of controlling the reboiler temperature is achieved.
The invention has the following beneficial effects:
when the temperature control system of the carbon dioxide capturing reboiler of the coal-fired power plant is operated specifically, a PID control mode is adopted according to the pressure of the regeneration tower and the temperature of the outlet of the reboiler, the temperature of the reboiler is adjusted by controlling the opening degree of the temperature regulating valve and the rotating speed of the reboiler pump, the operation is simple and convenient, the temperature of the reboiler can be effectively controlled, the energy consumption of the whole capturing system is further improved, and the practicability is strong.
Drawings
FIG. 1 is a schematic diagram of the present invention;
fig. 2 is a schematic diagram of the reboiler temperature controller 1.
Wherein, 1 is reboiler temperature controller, 2 is reboiler, 3 is regeneration tower, 4 is temperature regulating valve, 5 is reboiler pump, 6 is thermometer, 7 is pressure gauge, 8 is filtering module, 9 is adder, 10 is amplitude limiting module, 11 is manual/automatic switcher, 12 is PID controller, 13 is range controller, 14 is function module.
Detailed Description
In order to make the technical solutions of the present invention better understood, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, not all of the embodiments, and are not intended to limit the scope of the present disclosure. Moreover, in the following description, descriptions of well-known structures and techniques are omitted so as to not unnecessarily obscure the concepts of the present disclosure. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
There is shown in the drawings a schematic block diagram of a disclosed embodiment in accordance with the invention. The figures are not drawn to scale, wherein certain details are exaggerated and possibly omitted for clarity of presentation. The shapes of various regions, layers and their relative sizes and positional relationships shown in the drawings are merely exemplary, and deviations may occur in practice due to manufacturing tolerances or technical limitations, and a person skilled in the art may additionally design regions/layers having different shapes, sizes, relative positions, according to actual needs.
Referring to fig. 1, the temperature control system of the carbon dioxide capturing reboiler of the coal-fired power plant according to the present invention comprises a steam input pipeline, a temperature regulating valve 4, a reboiler, a regeneration tower 3, and a reboiler temperature controller 1;
the outlet at the bottom of the regeneration tower 3 is communicated with the inlet of the reboiler 2 through a reboiler pump 5, a pressure gauge 7 is arranged in the regeneration tower 3, a thermometer 6 is arranged at the outlet of the reboiler 2, the output end of the thermometer 6 and the output end of the pressure gauge 7 are connected with the input end of a reboiler temperature controller 1, and the output end of the reboiler temperature controller 1 is connected with the control end of a temperature regulating valve 4 and the control end of the reboiler pump 5.
Referring to fig. 2, the reboiler temperature controller 1 comprises a temperature setting correction value input terminal, a manual/automatic switching button, a reboiler temperature manual setting input terminal, a function module 14, a filter module 8, an adder 9, a limiting module 10, a manual/automatic switching device 11, a PID controller 12, and a split controller 13;
the output end of the pressure gauge 7 is connected with the input end of the function module 14, the output end of the function module 14 is connected with the input end of the filter module 8, the output end of the filter module 8 and the input end of the temperature setting correction value are connected with the input end of the adder 9, the output end of the adder 9 is connected with the input end of the amplitude limiting module 10, the output end of the amplitude limiting module 10 and the input end of the reboiler temperature manual setting are connected with the input end of the manual/automatic switcher 11, the manual/automatic switching button is connected with the control end of the manual/automatic switcher 11, the output end of the manual/automatic switcher 11 and the output end of the thermometer 6 are connected with the input end of the PID controller 12, the output end of the PID controller 12 is connected with the input end of the split-distance controller 13, and the output end of the split-distance controller 13 is connected with the control end of the temperature regulating valve 4 and the frequency converter of the reboiler pump 5.
The specific working process of the invention is as follows:
the operation mode of the manual/automatic switcher 11 is selected by the manual/automatic switching button;
when the manual/automatic switcher 11 is in the automatic control operation mode, the pressure gauge 7 measures the pressure information of the regeneration tower 3, the pressure information is calculated by the function module 14 to obtain temperature control target value information, the temperature control target value information is filtered by the filter module 8 to avoid the adjustment fluctuation caused by small pressure fluctuation, the filtered temperature control target value information and the temperature setting correction value are added by the adder 9, then the amplitude limiting processing is carried out by the amplitude limiting module 10, then the temperature control target value information and the temperature setting correction value are input into the manual/automatic switcher 11 as the target value of the outlet temperature of the reboiler 2, the target value of the outlet temperature of the reboiler 2 and the temperature at the outlet of the reboiler 2 measured by the thermometer 6 are processed by the PID controller 12, and then the result of the PID operation is input into the branch controller 13, finally, the opening degree of the temperature regulating valve 4 and the rotating speed of the reboiler pump 5 are controlled through the split controller 13, so that the temperature of the outlet of the reboiler 2 is consistent with the target value of the temperature of the outlet of the reboiler 2, and the aim of controlling the temperature of the reboiler 2 is fulfilled;
when the manual/automatic switching controller is in the manual control mode, a user inputs a target value of the reboiler 2 outlet temperature into the manual/automatic switching device 11 through the reboiler temperature manual setting input end, the target value of the reboiler 2 outlet temperature and the temperature at the reboiler 2 outlet measured by the thermometer 6 are subjected to PID operation through the PID controller 12, then the result of the PID operation is input into the split controller 13 for processing, and finally the split controller 13 controls the opening degree of the temperature regulating valve 4 and the rotating speed of the reboiler pump 5, so that the temperature at the reboiler 2 outlet is consistent with the target value of the reboiler 2 outlet temperature, and the aim of controlling the reboiler 2 temperature is achieved.

Claims (8)

1. A temperature control system of a carbon dioxide capturing reboiler of a coal-fired power plant is characterized by comprising a steam input pipeline, a temperature regulating valve (4), a reboiler, a regeneration tower (3) and a reboiler temperature controller (1);
the outlet at the bottom of the regeneration tower (3) is communicated with the inlet of the reboiler (2) through a reboiler pump (5), a thermometer (6) is arranged at the outlet of the reboiler (2), the output end of the thermometer (6) is connected with the input end of a reboiler temperature controller (1), and the output end of the reboiler temperature controller (1) is connected with the control end of a temperature regulating valve (4) and the control end of the reboiler pump (5).
2. The system for controlling the temperature of the carbon dioxide capturing reboiler of the coal fired power plant as recited in claim 1, wherein a pressure gauge (7) is provided in the regeneration tower (3), and an output end of the pressure gauge (7) is connected with an input end of the reboiler temperature controller (1).
3. The coal fired power plant carbon dioxide capture reboiler temperature control system of claim 2, wherein the reboiler temperature controller (1) comprises a temperature setting correction input, a manual/automatic switching button, a reboiler temperature manual setting input, a function module (14), a filter module (8), an adder (9), a limiting module (10), a manual/automatic switching device (11), a PID controller (12), and a split controller (13);
the output end of the pressure gauge (7) is connected with the input end of the function module (14), the output end of the function module (14) and the input end of the temperature setting correction value are connected with the input end of the adder (9), the output end of the adder (9) is connected with the input end of the amplitude limiting module (10), the output end of the amplitude limiting module (10) is connected with the input end of the PID controller (12), the output end of the PID controller (12) is connected with the input end of the split-range controller (13), and the output end of the split-range controller (13) is connected with the control end of the temperature regulating valve (4) and the frequency converter of the reboiler pump (5).
4. The carbon dioxide capture reboiler temperature control system for a coal fired power plant as recited in claim 1, characterized in that the output of function block (14) is connected to the input of filter block (8), and the output of filter block (8) and the temperature setting correction input are connected to the input of adder (9).
5. The coal fired power plant carbon dioxide capture reboiler temperature control system of claim 3, wherein the output of the limiting module (10) and the reboiler temperature manual setting input are connected to an input of a manual/automatic switch (11), and an output of the manual/automatic switch (11) is connected to an input of a PID controller (12).
6. The carbon dioxide capture reboiler temperature control system for a coal fired power plant as recited in claim 4, characterized in that a manual/automatic switching button is connected to a control end of the manual/automatic switching device (11).
7. The system for controlling the temperature of the carbon dioxide capturing reboiler in the coal fired power plant according to claim 3, wherein in operation, the pressure gauge (7) measures the pressure information of the regeneration tower (3), the pressure information is calculated by the function module (14) to obtain the temperature control target value information, the temperature control target value information is filtered by the filter module (8) to avoid the regulation fluctuation caused by the small fluctuation of the pressure, the filtered temperature control target value information and the temperature setting correction value are added by the adder (9), then the amplitude limiting processing is carried out by the amplitude limiting module (10), and then the filtered temperature control target value information and the temperature setting correction value are inputted into the manual/automatic switching device (11) as the target value of the outlet temperature of the reboiler (2), the target value of the outlet temperature of the reboiler (2) and the temperature at the outlet of the reboiler (2) measured by the thermometer (6) are PID operated by the PID controller (12), and then inputting the result of the PID operation into a split-range controller (13) for processing, and finally controlling the opening degree of the temperature regulating valve (4) and the rotating speed of the reboiler pump (5) through the split-range controller (13) to enable the temperature at the outlet of the reboiler (2) to be consistent with the target value of the temperature at the outlet of the reboiler (2).
8. The system for controlling the temperature of the carbon dioxide capturing reboiler of the coal-fired power plant as recited in claim 4, wherein a user inputs a target value of the outlet temperature of the reboiler (2) into the manual/automatic switching device (11) through a manual setting input end of the reboiler temperature, the target value of the outlet temperature of the reboiler (2) and the temperature at the outlet of the reboiler (2) measured by the thermometer (6) are subjected to PID operation through the PID controller (12), then the result of the PID operation is input into the split controller (13) to be processed, and finally the split controller (13) controls the opening degree of the temperature regulating valve (4) and the rotating speed of the reboiler pump (5) to enable the temperature at the outlet of the reboiler (2) to be consistent with the target value of the outlet temperature of the reboiler (2), so as to achieve the purpose of controlling the temperature of the reboiler (2).
CN202111153018.1A 2021-09-29 2021-09-29 Temperature control system of carbon dioxide capture reboiler of coal-fired power plant Active CN114397922B (en)

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Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012067101A1 (en) * 2010-11-16 2012-05-24 バブコック日立株式会社 Method and device for controlling system for chemically absorbing carbon dioxide
EP2481895A2 (en) * 2011-01-31 2012-08-01 Hitachi Ltd. Thermal power plant with carbon dioxide capture scrubbing equipment
CN103638780A (en) * 2013-11-26 2014-03-19 中国华能集团清洁能源技术研究院有限公司 Strengthening and regenerating system and method for carbon dioxide capturing solution
CN107450325A (en) * 2017-09-06 2017-12-08 东南大学 CO after one kind burning2The Multi model Predictive Controllers of trapping system
CN108710356A (en) * 2018-06-19 2018-10-26 东南大学 CO after the effective burning of one kind2Trap coal generating system progress control method
CN109188911A (en) * 2018-09-28 2019-01-11 东南大学 One kind is for CO after burning2The improvement INA feed forward control method of trapping system
CN110026068A (en) * 2019-04-08 2019-07-19 东南大学 A kind of large-scale coal fired power plant CO based on Neural network inverse control2Trapping system and feed forward control method
CN110152453A (en) * 2019-05-16 2019-08-23 清华大学 Use the method and apparatus of sour gas in solvent absorption captured gas mixture
CN111420516A (en) * 2020-04-24 2020-07-17 北京中冶设备研究设计总院有限公司 Steam waste heat cascade utilization system for carbon capture absorbent regeneration system
CN113341765A (en) * 2021-06-10 2021-09-03 江苏舜高智能科技有限公司 Coal-fired power plant CO for strictly controlling carbon emission2Flexible regulation and control method for trapping system

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012067101A1 (en) * 2010-11-16 2012-05-24 バブコック日立株式会社 Method and device for controlling system for chemically absorbing carbon dioxide
EP2481895A2 (en) * 2011-01-31 2012-08-01 Hitachi Ltd. Thermal power plant with carbon dioxide capture scrubbing equipment
CN103638780A (en) * 2013-11-26 2014-03-19 中国华能集团清洁能源技术研究院有限公司 Strengthening and regenerating system and method for carbon dioxide capturing solution
CN107450325A (en) * 2017-09-06 2017-12-08 东南大学 CO after one kind burning2The Multi model Predictive Controllers of trapping system
CN108710356A (en) * 2018-06-19 2018-10-26 东南大学 CO after the effective burning of one kind2Trap coal generating system progress control method
CN109188911A (en) * 2018-09-28 2019-01-11 东南大学 One kind is for CO after burning2The improvement INA feed forward control method of trapping system
CN110026068A (en) * 2019-04-08 2019-07-19 东南大学 A kind of large-scale coal fired power plant CO based on Neural network inverse control2Trapping system and feed forward control method
CN110152453A (en) * 2019-05-16 2019-08-23 清华大学 Use the method and apparatus of sour gas in solvent absorption captured gas mixture
CN111420516A (en) * 2020-04-24 2020-07-17 北京中冶设备研究设计总院有限公司 Steam waste heat cascade utilization system for carbon capture absorbent regeneration system
CN113341765A (en) * 2021-06-10 2021-09-03 江苏舜高智能科技有限公司 Coal-fired power plant CO for strictly controlling carbon emission2Flexible regulation and control method for trapping system

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
孟恩隆;贾成真;王灵梅;刘玉山;韩磊: "基于前馈和反馈的碳捕集智能控制技术研究", 《控制工程》 *

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Denomination of invention: A temperature control system for carbon dioxide capture reboiler in coal-fired power plants

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